|Publication number||US5234777 A|
|Application number||US 07/736,876|
|Publication date||Aug 10, 1993|
|Filing date||Jul 29, 1991|
|Priority date||Feb 19, 1991|
|Also published as||CA2080913A1, CA2080913C, DE69221881D1, DE69221881T2, EP0600888A1, EP0600888A4, EP0600888B1, WO1992015121A1|
|Publication number||07736876, 736876, US 5234777 A, US 5234777A, US-A-5234777, US5234777 A, US5234777A|
|Inventors||Mahlon S. Wilson|
|Original Assignee||The Regents Of The University Of California|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (5), Non-Patent Citations (8), Referenced by (176), Classifications (12), Legal Events (7)|
|External Links: USPTO, USPTO Assignment, Espacenet|
This application is a continuation-in-part of U.S. patent application Ser. No. 07/656,329, filed Feb. 19, 1991 now abandoned.
This invention relates to fuel cells and, more particularly, to catalyst loadings for solid polymer electrolyte fuel cells. This invention is the result of a contract with the Department of Energy (Contract No. W-7405-ENG-36).
Fuel cells are energy conversion devices presently being considered as one alternative to internal combustion engines. One type of fuel cell uses a solid polymer electrolyte (SPE) membrane, or proton exchange membrane, to provide ion exchange between the cathode and anode electrodes. Gaseous fuels may be used within the fuel cell, particularly hydrogen (H2) and oxygen (O2), where the electrodes are formed of porous conductive materials, e.g., woven graphite, to enable the fuel to disperse over the face of the SPE.
SPE fuel cells offer many advantages over liquid electrolyte fuel cells, including greater ultimate power densities, lower operating temperatures, and longer operating lifetimes. SPE materials are also generally resistant to corrosion and easy to incorporate into fuel cell structures. However, the anode and cathode half-cell reactions, H2 and O2 reactions, respectively, require catalysts to proceed at useful rates. As described in U.S. Pat. No. 4,876,115, issued Oct. 24, 1989, and incorporated herein by reference, catalyst materials were first incorporated by hot pressing the materials directly into the surface of the SPE membrane. Useful current densities in conventional SPE fuel cells were achieved only with high catalyst loadings, e.g., 4 mg Pt/cm2. Since the catalyst materials are from the platinum group, with platinum being the preferred catalyst, these SPE fuel cells (herein referred to as GE/HS-UTC-type fuel cells) have not been cost competitive with other energy sources.
The '115 patent is directed to reducing the required platinum loading where the platinum is provided as platinum loaded carbon particles on a carbon cloth or carbon paper electrode substrate bound together by a hydrophobic component, such as polytetrafluorethylene (PTFE). The catalyzed sides of the carbon electrodes are impregnated to a depth of about 10 μm with a solubilized form of the SPE to increase the access of the electrolyte to the platinum within the Pt-C/teflon catalyst layer. Indeed, catalyst loadings down to 0.35 mg/cm2 of SPE area are reported to provide performance equivalent to conventional fuel cell catalyst loadings of 4 mg/cm2.
The platinum catalyst is, however, not efficiently utilized in the prior art structures. It is difficult to match the impregnation depth of the SPE with the erratic thickness of a typical catalyst layer. This results in areas that are not fully impregnated and other areas where the SPE material extends deeper into the electrode than the catalyst layer and impedes gas diffusion through the electrode. Further, the hydrophobic binder blocks proton and oxygen access to catalyst sites in cathode electrodes.
Another problem with prior art fuel cells is differential swelling between the SPE and the catalyst layer arising from the differing hydration characteristics between the hydrophilic SPE membrane and the carbon-based electrode structure. Delamination can occur between the SPE membrane and the electrode with a resulting discontinuity in the ion path and decreased cell longevity.
These problems are addressed by the present invention and a catalyst layer is provided adjacent a fuel cell SPE that is hydrophilic, contains substantially no cavities, is uniformly thin, and contains a uniform ratio of binder ionomer to supported catalyst.
Accordingly, it is an object of the present invention to provide a SPE fuel cell with relatively low supported catalyst loadings with no reduction in performance.
It is another object of the present invention to provide uniform continuity of electronic and ionic paths about all of the catalyst sites.
Still another object of the present invention is to provide a uniform dispersion of the supported catalyst layer in the binder layer.
One other object of the present invention is to improve the bonding between the SPE membrane and the catalyst layer.
Yet another object of the present invention is to provide a thin catalyst layer for adequate oxygen transport to all the catalyst sites through the ionomer binder material.
Additional objects, advantages and novel features of the invention will be set forth in part in the description which follows, and in part will become apparent to those skilled in the art upon examination of the following or may be learned by practice of the invention. The objects and advantages of the invention may be realized and attained by means of the instrumentalities and combinations particularly pointed out in the appended claims.
To achieve the foregoing and other objects, and in accordance with the purposes of the present invention, as embodied and broadly described herein, the apparatus of this invention may comprise a solid polymer electrolyte (SPE) membrane assembly for separating anodic and cathodic electrodes backings for use in a gas reaction fuel cell, wherein the improvement comprises a SPE membrane and a film of a proton conducting material with a thickness less than about 10 μm and having a supported platinum catalyst uniformly dispersed therein with a platinum loading less than about 0.35 gm/cm2, where said film is bonded to the SPE membrane. A preferred film thickness is less than 5 μm.
In another characterization of the present invention, a SPE fuel cell using hydrogen and oxygen is formed with a SPE membrane assembly formed from a catalyst layer fabricated as a separate unit and bonded to a SPE membrane. A selected loading of supported Pt catalyst is uniformly dispersed in an ionomer that is effective for oxygen permeation and for ion transport, where the resulting mixture is formed as a thin film. The thin film is then transferred to the surface of a SPE membrane. The fuel cell is completed by urging a porous electrode structure against the catalyst film for oxygen transport through the ionomer to the catalyst sites.
In yet another characterization of the present invention, a SPE membrane assembly for use in a fuel cell using hydrogen and oxygen is formed using a Na+ form of a perfluorosulfonate ionomer to fabricate a catalyst layer. A supported Pt catalyst and a solvent are uniformly blended with the Na+ form of the ionomer to form an ink. The ink is applied to form a layer over a surface of a SPE membrane, also in the Na+ form. The layer is then dried at a temperature of at least 150° C. for a time effective to dry the ink. The resulting film and membrane are converted back to the protonated form of the ionomer to form a pliant, elastic, and coherent catalytic layer on the SPE membrane.
The accompanying drawings, which are incorporated and form a part of the specification, illustrate an embodiment of the present invention and, together with the description, serve to explain the principles of the invention. In the drawings:
FIG. 1 is a cross section of a fuel cell having a structure in accordance with one embodiment of the present invention.
FIG. 1A is a pictorial illustration showing a magnified view of the catalyst layer according to the present invention.
FIG. 2 graphically depicts the performance of a thin catalyst film with 0.20 mg/cm2 and a thicker catalyst film with 0.35 mg/cm2 of platinum on a first SPE.
FIG. 3 graphically compares performance of thin catalyst films with 0.15 and 0.22 mgPt/cm2 on a second SPE.
FIG. 4 graphically compares the performance of a thin film cathode according to the present invention with 0.15 mgPt/cm2 and a commercial gas-diffusion cathode with 0.35 mgPt/cm2.
FIG. 5 graphically depicts the performance of a fuel cell with a high-temperature formed, thin film catalyst layer with 0.17 gm Pt/cm2 /electrode on Membrane "C".
FIG. 6 graphically depicts the performance of a fuel cell with a high temperature formed, thin film catalyst layer with 0.13 mg Pt/cm2 /electrode on a Dow membrane.
FIG. 7 graphically compares the specific activity from a fuel cell according to the present invention and prior art fuel cells.
In accordance with the present invention, a gas reaction fuel cell includes a solid polymer electrolyte membrane assembly having a catalyst film adjacent the cathode surface of a solid polymer electrolyte membrane to optimize utilization of the catalyst and to minimize the amount of the included catalyst. A catalyst film may also be provided adjacent the anode surface of the solid polymer electrolyte membrane. As shown in FIGS. 1 and 1A, catalyst layer 22 addresses three criteria necessary for a catalyst to efficiently contribute to the electrochemical processes in a fuel cell: proton access to the catalyst, gas access, and electronic continuity.
Fuel cell assembly 10 utilizes a gas fuel source 12, gas oxidizer source 14, solid polymer electrolyte (SPE) membrane 26 between porous anode backing structure 16 and porous cathode backing structure 18, and at least catalyst layer according to the present invention, between the cathode surface of SPE 26 and cathode backing 18. It will be understood that catalyst layer 30 may be disposed between membrane and anode backing structure 16. Cathode backing structure 18 is electrically connected to cathode 34 and anode backing structure 16 is electrically connected to anode 32. The foregoing discussion applies also to catalyst layer 30, although catalyst loadings for the anode may be only about one-half the catalyst loadings required for the cathode structure. Catalyst layer 22 is formed as a film of an proton conductive ionomer 28 and a supported platinum (Pt) catalyst 24 uniformly dispersed in ionomer 28 to assure that a uniform and controlled depth of the catalyst is maintained. The resulting film is a dense film of ionomer 28 and supported catalyst i.e., there are no substantial voids in the film and there are no hydrophobic additives, such as PTFE, that block access of the diffusing gas and protons to the Pt catalyst sites. Gas access to the Pt catalyst sites is obtained through porous cathode backing structure 18 and by diffusion through ionomer 28. A suitable ionomer, such as a perfluorosulfonate ionomer, has sufficient oxygen permeability that a diffusion pathway length of 5-10 μm does not introduce any significant oxygen transport losses through the film for an oxygen gas.
Proton penetration and gas diffusion effects of electrolyte layers, as well as the relationship between volume fraction of ionomer 28 and potential drop within catalyst layer 22, indicate that an optimum catalyst layer 22 is very thin, i.e., a film less than 10 μm, thick and has a high volume density of supported catalyst 24 with the ionomer 28 in the interstices, i.e., the supporting carbon particles 25 are in contact with adjacent particles to form a low resistance electronic path through catalyst layer 22. A weight ratio of about 1:3 perfluorosulfonate ionomer (dry)/Pt-C is preferred for 20 wt % supported Pt. A dense film 22 is formed that is substantially free of cavities or water pockets that will lower the ionic and electronic conductivities. It will be appreciated that the thickness of film 22 is optimized when the thickness is equal to the active region for the half-cell reaction at any given current density and may be selected on the basis of the expected operating characteristics to match the catalyst thickness with a predetermined operating current density.
In one embodiment, film is formed from an ink preparation including the supported catalyst, a solubilized ionomer, and one or more volatile or decomposable suspension materials to provide a viscosity suitable for film formation. The ink is spread over a release blank in one or more layers to provide a preselected concentration of catalyst. A preferred protocol is as follows:
1. Combine a solubilized perfluorosulfonate ionomer, such as Nafion (a registered trademark of E.I. duPont Nemours) in 5% solution (from Solution Technology, Inc.) and a supported catalyst (19.8 wt % platinum on carbon from Prototech Company, Newton Highlands, Mass.) in a weight ratio of 1:3 Nafion (dry)/Pt-C.
2. Add water and glycerol to weight ratios of about 1:5:20 for carbon/water/glycerol.
3. Agitate the mixture with ultrasound to uniformly disperse the supported catalyst in the ink and to form the mixture to a viscosity suitable for coating the release blank.
4. Clean a release blank of teflon film and coat the blank with a thin layer of mold release (e.g., a TFE spray). Paint the blank with a layer of ink and bake in an oven at 135° C. until dry. Add layers until the desired catalyst loading is achieved.
5. Form an assembly of a polymer electrolyte membrane, counter electrode (anode electrode), and the coated blank. Place the assembly into a conventional hot press and lightly load the press until the press heats to a selected temperature (i.e., 125° C. for "Nafion" and 145° C. for "C" SPE material) and then press at 70-90 atm for 90 seconds.
6. Cool the assembly and then release blank from the film, leaving the film adhered to the SPE membrane cathode surface.
7. An uncatalyzed porous electrode (Prototech) is urged against the films during fuel cell assembly to form a gas diffusion backing for the thin film catalyst layer.
It should be recognized that the solubilized "Nafion" acts to some extent as a surfactant and dispersing agent for the supported catalyst particles. However, the dispersion of the "Nafion" must be controlled to provide a suitably dense film. An effective density for the present invention is obtained, by simply mixing the Pt-C particles and solubilized "Nafion" together before the water and glycerol mixture is added.
One advantage of the dense catalyst film herein described is improved bonding of the catalyst, film to the SPE membrane and continuity of the proton path. The dimensions of the SPE membrane increase considerably upon hydration of the hydrophilic material, whereas the relatively rigid carbon matrix of conventional gas-diffusion electrode structures does not significantly change dimensions upon hydration. Thus, where the catalyst is included within the carbon electrode structure, the continuity between the SPE surface and the catalyst interface can be adversely affected. The dense catalyst film according to the present invention includes a hydrophilic material as a large fraction of the catalyst film and there is less differential movement from surface expansions under hydration.
One disadvantage of forming the catalyst film without a binder material, such as PTFE, is that suitable ionomer materials, such as "Nafion", must provide structural integrity for the film. Nafion, for example, is not melt processable and the resulting recast catalyst layer films do not have the structural integrity of commercial fluoropolymer SPE membranes. It has been found, however, that the structural integrity can be improved by heating the film to elevated temperatures for moderate amounts of time. This does cause some amount of acid-catalyzed discoloration and degradation, but the increase in structural integrity is beneficial. The film is also rendered somewhat less hydrophilic by the heating, which is beneficial at the cathode electrode where water flooding is of concern. A suitable treatment is thirty minutes exposure at 130°-135° C.
Another approach to improve the structural integrity of the catalyst layer film is to introduce a binder material that readily disperses throughout the electrode structure and imparts structural integrity at low volume fractions such that performance of the electrode is not significantly impaired. Useful catalyst layers have been prepared using polyvinyl alcohol (PVA) in place of the glycerol in forming the ink. The surfactant nature of the PVA provides for adequate dispersion among the supported catalyst particles and the molecular structure acts to bind the carbon particles and "Nafion" agglomerates so that strong films are obtained with low weight fractions of PVA. Films have been formed with PVA concentrations of 10-12 wt % in the ink.
In another embodiment of the present invention, the integrity of catalyst films 22, 30 is improved and acid-catalyzed degradation of the ionomer is avoided by using the Na+ form of the perfluorosulfonate ionomer, i.e., "Nafion", to form a film for application to membrane 26 or for direct application to membrane 26, where membrane 26 is in a Na+ or K+ form. The Na+ perfluorosulfonate layer is cured at a temperature of at least 150° C., and preferably at least 160° C., and the catalyzed membrane assembly is thereafter converted to the H+, i.e., protonated, form to complete the catalyzed membrane assembly. A preferred protocol is as follows:
1. Prepare a mixture of "Nafion" and catalyst as described in Step 1 of Protocol I.
2. Add a molar amount, of NaOH equal to the "Nafion" and mix well to convert the "Nafion" to the Na+ form.
3. Form an ink as in steps 2 and 3 of Protocol I.
4. Provide a membrane of Na+ "Nafion" by soaking a protonated membrane in a solution of NaOH, followed by rinsing and drying, or by procuring the membrane in a Na+ or K+ form.
5. Apply the ink directly to one side of the membrane. The amount of catalyst applied to the membrane is determined from the amount of ink transferred to the surface. Typically, two coats are required to obtain the desired catalyst loading. In one method of drying the ink, the ink-coated membrane is placed on a vacuum table having a fine sintered stainless steel filter on top of a heated vacuum manifold plate. A silicone blanket having a cut-out area the size of the membrane area to be inked is placed over the membrane to seal the uncovered areas of the vacuum table about the membrane. The vacuum table is operated at a temperature of at least 150° C., and preferably about 160° C., as the ink is applied. The vacuum appears to prevent distortion of the membrane from solvents in the ink and to yield a smooth, uniform film. The high-temperature application and drying appears to cure the catalyst layer to a film of high integrity and that is pliant and elastic. The second side of the membrane may be coated in the same manner.
6. Optionally, the assembly is hot pressed at 70-90 atm at 185° C. for about 90 seconds.
7. The assembly is converted back to the protonated form by lightly boiling it in 0.1M H2 SO4 and rinsing in deionized water. The assembly is air dried and combined with an uncatalyzed porous electrode as in Step 7 of Protocol I.
Alternately, the Na+ form of ink (Steps 1-3, above) and membrane may be used in Protocol I to form a separate catalyst film for application to the membrane.
The high-temperature casting of Na+ "Nafion" films to improve film integrity is generally suggested in Moore et al., "Procedure for Preparing Solution-Cast Perfluorosulfonate Ionomer Films and Membranes," 58 Anal. Chem., pp. 2569-2570 (1986), incorporated herein by reference. The article suggests that solvents such as dimethyl sulfoxide (DMSO) might yield equivalent properties to glycerol solvents, described above, but at lower process temperatures. The above protocol appears to yield equivalent cell performance with both DMSO and glycerol solvents DMSO does provide a good suspension medium for the solids, however, and may form a good solution for a spray application of ink to the membrane surface.
FIGS. 2-7 graphically depict the performance of fuel cells prepared according to the present invention. All of the ink formulations were prepared using supported catalysts of 19.8 wt % platinum on XC-72 carbon powder (Prototech) mixed with "Nafion". The cathode electrodes for mating with the catalyst layer were conventional PTFE bonded electrodes with no catalyst (Prototech). The fuel cells whose performance is shown in FIGS. 1-4 have cathodes prepared according to Protocol I and include conventional anodes (Prototech) with a catalyst loading of 0.35 mg Pt/cm2 plus a sputter coat of 500 Å Pt. It will be understood that conventional anode electrodes were used to provide performance comparisons of cathode electrodes.
The anode catalyst loading is not expected to have any significant effect on cell performance, Indeed, the fuel cells whose performance is shown in FIGS. 5 and 6 include high temperature catalytic layers on both the cathode and anode faces of the membrane. Both catalytic layers incorporated equivalent catalyst loadings, e.g., 0.13 mg Pt/cm2, for a total cell loading of 0.26 mg Pt/cm2 of electrode surface.
FIG. 2 graphically depicts the voltage vs. current density curves for fuel cells having conventional Prototech anodes, "Nafion" 117 (7 mil thick) SPE membrane, and a cathode assembly with a catalyst layer produced by mixing Pt/C catalyst and "Nafion" and hot pressed onto the SPE membrane. Catalyst loadings of 0.20 and 0.35 mg Pt/cm2 are compared using both neat oxygen and air as the oxidant. It is readily seen that the thinner catalyst layer (0.20 mg Pt/cm2) performs somewhat better than the thicker film (0.35 mg Pt/cm2) at higher current densities. At the higher current densities, the active region of the catalyst layer narrows and less of the film thickness is utilized, wherein mass transfer losses increase in the thicker film and performance decreases. The low partial pressure of oxygen in air as compared to neat oxygen induces an earlier and steeper fall off in performance at the higher current densities.
FIG. 3 graphically depicts the voltage vs. current density curves for fuel cells constructed as the fuel cells of FIG. 2, except that the SPE membrane is Membrane "C" (a perfluorosulfonate membrane from Chlorine Engineers Inc. of Japan). Catalyst loadings of 0.15 and 0.22 mg Pt/cm2 are compared, again using both neat oxygen and air as oxidizers. The results, are consistent with the results shown with "Nafion 117" forming the SPE membrane, with lower potentials from the thicker film at higher current densities.
The performance of the fuel cells depicted in both FIGS. 2 and 3 approach those of fuel cells fabricated with conventional Prototech cathode assemblies or of assemblies using unsupported Pt catalyst with much higher Pt loadings FIG. 4 particularly compares the cell voltage vs. current density performance of a thin catalyst with a loading of 0.15 mg Pt/cm2 with a cell having the catalyst included in a carbon electrode to a loading of 0.35 mg Pt/cm2 with an extra sputter coating of 500 Å Pt. The substantial similarity in performance is readily apparent.
The performance of fuel cells formed by a direct application of a Na+ ink to a Na+ membrane is shown in FIGS. 5 and 6. FIG. 5 depicts the performance of the high-temperature, thin film formed on Membrane "C" according to Protocol II, wherein the cell performance on oxygen is at least equal to the performance of the separate thin film cell shown in FIG. 4. FIG. 6 depicts the performance of the high-temperature, thin film formed on a "Dow" membrane according to Protocol II, wherein an improved cell performance is obtained. The "Dow" membrane is a proton conducting membrane available from the Dow Chemical Company. It is quite significant that a low Pt loading of 0.13 mg Pt/cm2 is effective to generate current densities of above 3 A/cm2 at a cell voltage higher than 0.4 V for operation on pressurized oxygen and, particularly, that such a low loading is effective to reach a cell voltage of 0.65 V at 1 A/cm2 for cells operated on pressurized air.
To further illustrate the significant increase in catalyst utilization efficiency afforded by the present invention, FIG. 7 depicts cell voltage as a function of the specific activities of the cathodes (A/mgPt) for fuel cells with four different cathode catalyst configurations: (1) a thin film catalyst loading of 0.15 mg Pt/cm2, as taught herein; (2) a high-temperature thin film with a catalyst loading of 0.13 mg Pt/cm2 applied directly to the membrane as an ink; (3) a commercial Prototech electrode with a catalyst loading of 0.35 mg Pt/cm2 and 500 Å Pt coating; and (4) GE/HS-UTC-type cell with 4 mg Pt/cm2 (unsupported) hot pressed into the SPE. It should be noted that the GE/HS-UTC-type cell has hardware, membrane design, and operating conditions that are significantly different from the other cells and its performance comparison is merely illustrative. The differences in the specific activities for each type of electrode are clearly significant, with the thin film supported catalyst layers according to the present invention being the most efficient utilization of the Pt catalyst.
Thus, it will be appreciated that the present invention obtains a high catalyst utilization by the improved construction of the catalyst layer with low Pt loadings primarily involving increased contact area between the polymer electrolyte and the Pt catalyst clusters. The contact area is increased in two ways. First, the supported catalyst and the ionomeric additive are cast together to form the catalytic layer. Second, the hydrophobic additive is completely eliminated and the ionomer is uniformly dispersed throughout the catalyst layer. The latter is accomplished by blending the solubilized ionomer and the platinized carbon into a homogeneous "ink," from which the thin film catalyst layer is formed.
FIGS. 2 and 3 illustrate the significance of film thickness affecting proton penetration and gas access and the resulting cell performance. As current density increases, the active catalyst region narrows. Thus, the oxidizer gas must diffuse through the inactive portion of the catalyst layer and, in the case of air, the mass transfer limitation significantly increases the overpotential. An electrode thickness roughly equivalent to that of the active region at a particular current density would provide an optimum performance at that current density. For example, with 20 wt % Pt/C. supported catalyst and a catalyst layer fabricated in accordance with the above principles, reasonable fuel cell performance is obtained down to about 0.1 mg Pt/cm2, after which it falls off in proportion to further decrease in catalyst loading. Concomitant film thicknesses are in the range of 1-10μ, and preferably 2 to 3μ. It is expected that catalyst loadings as low as 0.05 mg Pt/cm2 may be used for an anode catalyst layer without significant loss of performance. Improved performance might be obtained from a given catalyst layer thickness if a higher Pt loading could be included without increasing the thickness of the supported catalyst.
The foregoing description of the preferred embodiments of the invention have been presented for purposes of illustration and description. It is not intended to be exhaustive or to limit the invention to the precise form disclosed, and obviously many modifications and variations are possible in light of the above teaching. The embodiments were chosen and described in order to best explain the principles of the invention and its practical application to thereby enable others skilled in the art to best utilize the invention in various embodiments and with various modifications as are suited to the particular use contemplated. It is intended that the scope of the invention be defined by the claims appended hereto.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US4215183 *||Jan 2, 1979||Jul 29, 1980||General Electric Company||Wet proofed conductive current collector for the electrochemical cells|
|US4262063 *||May 22, 1979||Apr 14, 1981||Hitachi, Ltd.||Fuel cell using electrolyte-soluble fuels|
|US4369103 *||Aug 14, 1981||Jan 18, 1983||Ppg Industries, Inc.||Solid polymer electrolyte cell|
|US4804592 *||Oct 16, 1987||Feb 14, 1989||The United States Of America As Represented By The United States Department Of Energy||Composite electrode for use in electrochemical cells|
|US4876115 *||Mar 3, 1988||Oct 24, 1989||United States Department Of Energy||Electrode assembly for use in a solid polymer electrolyte fuel cell|
|1||A. K. Shukla et al., "A Nafion'-Bound Platinized Carbon Electrode For Oxygen Reduction In Solid Polymer Electrolyte Cells," 19 J. Appl. Electrochem., pp. 383-386 (1989).|
|2||*||A. K. Shukla et al., A Nafion Bound Platinized Carbon Electrode For Oxygen Reduction In Solid Polymer Electrolyte Cells, 19 J. Appl. Electrochem., pp. 383 386 (1989).|
|3||C. Liu et al., "Ion-Transporting Composite Membranes," 137 J. Electrochem. Soc., No. 10, pp. 3114-3120 (Oct. 1990).|
|4||*||C. Liu et al., Ion Transporting Composite Membranes, 137 J. Electrochem. Soc., No. 10, pp. 3114 3120 (Oct. 1990).|
|5||P. Aldebert, "Preparation and Characterization of SPE Composites for Electrolyzers and Fuel Cells," Solid State Ionics 35:3 (1989).|
|6||*||P. Aldebert, Preparation and Characterization of SPE Composites for Electrolyzers and Fuel Cells, Solid State Ionics 35:3 (1989).|
|7||R. B. Moore et al., "Procedure for Preparing Solution-Cast Perfluorosulfonate Ionomer Films and Membranes," 58 Anal. Chem. pp. 2569-2570 (1986).|
|8||*||R. B. Moore et al., Procedure for Preparing Solution Cast Perfluorosulfonate Ionomer Films and Membranes, 58 Anal. Chem. pp. 2569 2570 (1986).|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US5470448 *||Jan 28, 1994||Nov 28, 1995||United Technologies Corporation||High performance electrolytic cell electrode/membrane structures and a process for preparing such electrode structures|
|US5472799 *||Sep 22, 1993||Dec 5, 1995||Tanaka Kikinzoku Kogyo K.K.||Solid polymer electrolyte fuel cell|
|US5523177 *||Oct 12, 1994||Jun 4, 1996||Giner, Inc.||Membrane-electrode assembly for a direct methanol fuel cell|
|US5538585 *||May 18, 1994||Jul 23, 1996||Permelec Electrode Ltd.||Process for producing gas electrode|
|US5595834 *||Jan 17, 1996||Jan 21, 1997||The Regents Of The University Of Calif.||Annular feed air breathing fuel cell stack|
|US5620807 *||Aug 31, 1995||Apr 15, 1997||The Dow Chemical Company||Flow field assembly for electrochemical fuel cells|
|US5631099 *||Sep 21, 1995||May 20, 1997||Hockaday; Robert G.||Surface replica fuel cell|
|US5639516 *||Jun 5, 1995||Jun 17, 1997||Vlaamse Instelling Voor Technologisch Onderzoek||Method for making a gas diffusion electrode|
|US5641586 *||Dec 6, 1995||Jun 24, 1997||The Regents Of The University Of California Office Of Technology Transfer||Fuel cell with interdigitated porous flow-field|
|US5695873 *||Jun 5, 1995||Dec 9, 1997||The University Of Dayton||Polymer-ceramic composite electrolytes|
|US5702755 *||Nov 6, 1995||Dec 30, 1997||The Dow Chemical Company||Process for preparing a membrane/electrode assembly|
|US5716664 *||Jun 19, 1996||Feb 10, 1998||Marchetti; George A.||Method of making a hydrophilic, graphite electrode membrane assembly|
|US5716680 *||Apr 1, 1996||Feb 10, 1998||The Dow Chemical Company||Solventless process for forming thin, durable coatings of perfluorocarbon ionomers on various polymeric materials|
|US5738905 *||Mar 15, 1996||Apr 14, 1998||Deutsche Forschungsanstalt Fuer Luft- Und Raumfahrt E.V.||Process for the production of a composite comprising electrode material, catalyst material and a solid-electrolyte membrane|
|US5759712 *||Jan 6, 1997||Jun 2, 1998||Hockaday; Robert G.||Surface replica fuel cell for micro fuel cell electrical power pack|
|US5798036 *||Jun 28, 1996||Aug 25, 1998||E. I. Du Pont De Nemours And Company||Electrochemical conversion of anhydrous hydrogen halide to halogens gas using a membrane-electrode assembly or gas diffusion electrodes|
|US5800938 *||Dec 4, 1995||Sep 1, 1998||Tanaka Kikinzoku Kogyo K.K.||Sandwich-type solid polymer electrolyte fuel cell|
|US5869201 *||Dec 22, 1995||Feb 9, 1999||George Marchetti||Hydrophilic, graphite fuel cell electrode for use with an ionomer membrane|
|US5869202 *||May 21, 1997||Feb 9, 1999||George A. Marchetti||Hydrophillic graphite fuel cell electrode for use with an ionomer membrane fuel cell|
|US5869416 *||Jul 31, 1997||Feb 9, 1999||The Dow Chemical Company||Electrode ink for membrane electrode assembly|
|US5882810 *||Mar 7, 1997||Mar 16, 1999||The Dow Chemicalcompany||Active layer for membrane electrode assembly|
|US5885729 *||Jun 18, 1997||Mar 23, 1999||George A. Marchetti||Hydrophilic, graphite fuel cell electrode for use with an ionomer membrane and method of making a fuel cell.|
|US5952119 *||Feb 24, 1997||Sep 14, 1999||Regents Of The University Of California||Fuel cell membrane humidification|
|US5958616 *||Feb 6, 1998||Sep 28, 1999||Lynntech, Inc.||Membrane and electrode structure for methanol fuel cell|
|US6030718 *||Nov 20, 1997||Feb 29, 2000||Avista Corporation||Proton exchange membrane fuel cell power system|
|US6054230 *||Dec 6, 1995||Apr 25, 2000||Japan Gore-Tex, Inc.||Ion exchange and electrode assembly for an electrochemical cell|
|US6096449 *||Jul 1, 1998||Aug 1, 2000||Avista Labs||Fuel cell and method for controlling same|
|US6103412 *||May 12, 1998||Aug 15, 2000||Mazda Motor Corporation||Polymer electrolyte fuel cell|
|US6106965 *||Mar 31, 1997||Aug 22, 2000||Mazda Motor Corporation||Polymer electrolyte fuel cell|
|US6131851 *||Jun 2, 1998||Oct 17, 2000||Lockheed Martin Corporation||Apparatus having an energy generating skin as an outer covering|
|US6136389 *||Dec 18, 1998||Oct 24, 2000||Amt Holdings, Inc.||Preparation of metal coatings|
|US6156449 *||Aug 18, 1999||Dec 5, 2000||Degussa-Huls Aktiengellschaft||Catalyst layer for polymer electrolyte fuel cells|
|US6180163||Jan 12, 1999||Jan 30, 2001||E. I. Du Pont De Nemours And Company||Method of making a membrane-electrode assembly|
|US6194095||Dec 15, 1998||Feb 27, 2001||Robert G. Hockaday||Non-bipolar fuel cell stack configuration|
|US6203675||Jun 9, 1998||Mar 20, 2001||E. I. Du Pont De Nemours And Company||Electrochemical conversion of anhydrous hydrogen halide to halogen gas using an electrochemical cell|
|US6218035||Dec 21, 1999||Apr 17, 2001||Avista Laboratories, Inc.||Proton exchange membrane fuel cell power system|
|US6277513||Apr 12, 1999||Aug 21, 2001||General Motors Corporation||Layered electrode for electrochemical cells|
|US6284401||May 19, 1999||Sep 4, 2001||George A. Marchetti||Thin graphite bipolar plate with associated gaskets and carbon cloth flow-field for use in an ionomer membrane fuel cell|
|US6287717||Nov 13, 1998||Sep 11, 2001||Gore Enterprise Holdings, Inc.||Fuel cell membrane electrode assemblies with improved power outputs|
|US6300000||Jun 18, 1999||Oct 9, 2001||Gore Enterprise Holdings||Fuel cell membrane electrode assemblies with improved power outputs and poison resistance|
|US6309772||Mar 22, 1999||Oct 30, 2001||Degussa Ag||Membrane-electrode unit for polymer electrolyte fuel cells and processes for their preparation|
|US6312845||May 23, 1997||Nov 6, 2001||The Dow Chemical Company||Macroporous flow field assembly|
|US6326097||Dec 10, 1998||Dec 4, 2001||Manhattan Scientifics, Inc.||Micro-fuel cell power devices|
|US6376111||Jan 25, 2000||Apr 23, 2002||General Motors Corporation||System and method for controlling the humidity level of a fuel cell|
|US6426126||Oct 21, 2000||Jul 30, 2002||Amt Holdings, Inc.||Preparation of metal coatings|
|US6428896||Jun 17, 1998||Aug 6, 2002||Ut-Battelle, Llc||Low temperature material bonding technique|
|US6465136||Apr 28, 2000||Oct 15, 2002||The University Of Connecticut||Membranes, membrane electrode assemblies and fuel cells employing same, and process for preparing|
|US6468682||May 17, 2000||Oct 22, 2002||Avista Laboratories, Inc.||Ion exchange membrane fuel cell|
|US6500571||Aug 18, 1999||Dec 31, 2002||Powerzyme, Inc.||Enzymatic fuel cell|
|US6521381||Mar 16, 1999||Feb 18, 2003||General Motors Corporation||Electrode and membrane-electrode assemblies for electrochemical cells|
|US6524736||Oct 18, 2000||Feb 25, 2003||General Motors Corporation||Methods of preparing membrane electrode assemblies|
|US6555261||Oct 29, 1999||Apr 29, 2003||3M Innovative Properties Company||Microstructured flow fields|
|US6602630 *||Mar 13, 2001||Aug 5, 2003||The Electrosynthesis Company, Inc.||Membrane electrode assemblies for electrochemical cells|
|US6613203||Sep 10, 2001||Sep 2, 2003||Gore Enterprise Holdings||Ion conducting membrane having high hardness and dimensional stability|
|US6630263||Nov 20, 2000||Oct 7, 2003||Plug Power Inc.||Fuel cell systems and methods|
|US6638659||Sep 12, 2000||Oct 28, 2003||University Of Connecticut||Membrane electrode assemblies using ionic composite membranes|
|US6696382||Nov 14, 2000||Feb 24, 2004||The Regents Of The University Of California||Catalyst inks and method of application for direct methanol fuel cells|
|US6703076 *||Oct 14, 2000||Mar 9, 2004||Forschungszentrum Julich Gmbh||Production of catalyst layers on diaphragms for low-temperature fuel cells|
|US6743536||Jul 26, 2001||Jun 1, 2004||Relion, Inc.||Fuel cell power system and method of controlling a fuel cell power system|
|US6749892||Mar 21, 2001||Jun 15, 2004||Samsung Electronics Co., Ltd.||Method for fabricating membrane-electrode assembly and fuel cell adopting the membrane-electrode assembly|
|US6770394||Feb 8, 2001||Aug 3, 2004||The Texas A&M University System||Fuel cell with monolithic flow field-bipolar plate assembly and method for making and cooling a fuel cell stack|
|US6828054||Feb 8, 2001||Dec 7, 2004||The Texas A&M University System||Electronically conducting fuel cell component with directly bonded layers and method for making the same|
|US6828056||Sep 27, 2001||Dec 7, 2004||Proton Energy Systems, Inc.||Electrode catalyst composition, electrode, and membrane electrode assembly for electrochemical cells|
|US6833212||Mar 29, 2002||Dec 21, 2004||Hewlett-Packard Development Company, L.P.||Electrolyte for a fuel cell|
|US6933003||Jun 13, 2002||Aug 23, 2005||General Motors Corporation||Method of making membrane electrode assemblies|
|US7005206||May 31, 2002||Feb 28, 2006||Polyfuel, Inc.||Fuel cell assembly for portable electronic device and interface, control, and regulator circuit for fuel cell powered electronic device|
|US7041401 *||Oct 20, 2003||May 9, 2006||University Of Iowa Research Foundation||Magnetically modified electrodes containing at least one catalyst component that mediates a subatomic particle transfer process|
|US7052805||Jun 1, 2001||May 30, 2006||Sri International||Polymer electrolyte having acidic, basic and elastomeric subunits|
|US7056612||Dec 23, 2002||Jun 6, 2006||Hyundai Motor Company||Method of preparing membrane-electrode-gasket assemblies for polymer electrolyte fuel cells|
|US7094490||May 13, 2003||Aug 22, 2006||Polyfuel, Inc.||Ion conductive block copolymers|
|US7108773||Sep 11, 2002||Sep 19, 2006||The Board Of Trustees Of The University Of Illinois||Solids supporting mass transfer for fuel cells and other applications and solutions and methods for forming|
|US7125626||Feb 26, 2003||Oct 24, 2006||Japan Gore-Tex, Inc.||Ion exchange assembly for an electrochemical cell|
|US7153802||Apr 7, 2004||Dec 26, 2006||Proton Energy Systems, Inc.||Method of making an electrode for a membrane electrode assembly and method of making the membrane electrode assembly|
|US7202001||May 13, 2003||Apr 10, 2007||Polyfuel, Inc.||Sulfonated copolymer|
|US7226689||Jun 20, 2003||Jun 5, 2007||Ballard Power Systems Inc.||Method of making a membrane electrode assembly for electrochemical fuel cells|
|US7258945||Nov 26, 2003||Aug 21, 2007||Utc Power Corporation||Fuel cell having a hydrophilic substrate layer|
|US7291419||Jan 22, 2004||Nov 6, 2007||General Motors Corporation||Durable membrane electrode assembly catalyst coated diffusion media with no lamination to membrane|
|US7316855||Dec 3, 2002||Jan 8, 2008||Polyfuel, Inc.||Fuel cell assembly for portable electronic device and interface, control, and regulator circuit for fuel cell powered electronic device|
|US7326487||Oct 15, 2003||Feb 5, 2008||Samsung Sdi Co., Ltd.||Method for fabricating membrane-electrode assembly and fuel cell adopting the membrane-electrode assembly|
|US7354679||Nov 12, 2004||Apr 8, 2008||Polyfuel, Inc.||Ion conductive random copolymers|
|US7419740||Jul 19, 2001||Sep 2, 2008||Unicore Ag & Co. Kg||Membrane electrode unit for polymer electrolyte fuel cells and a process for the production thereof|
|US7541308||Mar 29, 2002||Jun 2, 2009||Cabot Corporation||Fuel cells and other products containing modified carbon products|
|US7824788||Mar 15, 2006||Nov 2, 2010||Solvay Solexis S.P.A.||CCM composite|
|US7931995||Sep 9, 2003||Apr 26, 2011||Gore Enterprise Holdings, Inc.||Solid electrolyte composite for electrochemical reaction apparatus|
|US7947410||Aug 22, 2008||May 24, 2011||Toyota Motor Engineering & Manufacturing North America, Inc.||Fuel cell electrodes with triazole modified polymers and membrane electrode assemblies incorporating same|
|US7955758||Jan 22, 2004||Jun 7, 2011||GM Global Technology Operations LLC||Membrane electrode assembly prepared by direct spray of catalyst to membrane|
|US8003274||Oct 25, 2007||Aug 23, 2011||Relion, Inc.||Direct liquid fuel cell|
|US8026020||May 8, 2007||Sep 27, 2011||Relion, Inc.||Proton exchange membrane fuel cell stack and fuel cell stack module|
|US8061651 *||Feb 14, 2008||Nov 22, 2011||Lockheed Martin Corporation||Airship photocatalytic reactor energy generation, storage, and pipeless transmission systems|
|US8124261||Jun 20, 2006||Feb 28, 2012||Basf Corporation||Process for recycling components of a PEM fuel cell membrane electrode assembly|
|US8142957||Oct 12, 2006||Mar 27, 2012||Byd Company Ltd||Method for preparing a membrane electrode of a fuel cell|
|US8187764 *||Feb 6, 2006||May 29, 2012||Samsung Sdi Co., Ltd.||Fuel cell with moisture retentive layer in MEA|
|US8268464||Sep 24, 2010||Sep 18, 2012||Solvay Solexis S.P.A.||CCM composite|
|US8372237||Dec 27, 2006||Feb 12, 2013||Solvay Solexis S.P.A.||Process for obtaining CCM with subgaskets|
|US8597846||Apr 26, 2012||Dec 3, 2013||Relion, Inc.||Proton exchange membrane fuel cell stack and fuel cell stack module|
|US8758953||Mar 21, 2011||Jun 24, 2014||Trenergi Corp.||High temperature membrane electrode assembly with high power density and corresponding method of making|
|US8993472||Nov 6, 2009||Mar 31, 2015||National Research Council Of Canada||Catalytic materials for fuel cell electrodes and method for their production|
|US9012108||Apr 25, 2011||Apr 21, 2015||Toyota Motor Engineering & Manufacturing North America, Inc.||Fuel cell electrodes with triazole modified polymers and membrane electrode assemblies incorporating same|
|US9240606||May 6, 2014||Jan 19, 2016||Trenergi Corp.||High temperature membrane electrode assembly with high power density and corresponding method of making|
|US9293778||Jun 11, 2007||Mar 22, 2016||Emergent Power Inc.||Proton exchange membrane fuel cell|
|US9735441 *||Sep 30, 2010||Aug 15, 2017||Audi Ag||Hot pressed, direct deposited catalyst layer|
|US20020037449 *||Jul 19, 2001||Mar 28, 2002||Matthias Binder||Membrane electrode unit for polymer electrolyte fuel cells and a process for the production thereof|
|US20030017379 *||Mar 29, 2002||Jan 23, 2003||Jameel Menashi||Fuel cells and other products containing modified carbon products|
|US20030039868 *||Aug 23, 2002||Feb 27, 2003||Liberatore Michael James||Enzymatic fuel cell|
|US20030113604 *||Oct 25, 2002||Jun 19, 2003||Bamdad Bahar||Fuel cell comprising a composite membrane|
|US20030121603 *||Dec 23, 2002||Jul 3, 2003||In-Whan Oh||Method of preparing membrane-electrode-gasket assemblies for polymer electrolyte fuel cells|
|US20030152820 *||Feb 26, 2003||Aug 14, 2003||Hiroshi Kato||Ion exchange assembly for an electrochemical cell|
|US20030186108 *||Mar 29, 2002||Oct 2, 2003||Yoocharn Jeon||Electrolyte for a fuel cell|
|US20030232714 *||Jun 13, 2002||Dec 18, 2003||Yan Susan G.||Method of making membrane electrode assemblies|
|US20040036394 *||Aug 21, 2002||Feb 26, 2004||3M Innovative Properties Company||Process for preparing multi-layer proton exchange membranes and membrane electrode assemblies|
|US20040045814 *||Sep 9, 2003||Mar 11, 2004||Bamdad Bahar||Solid electrolyte composite for electrochemical reaction apparatus|
|US20040045816 *||Sep 11, 2002||Mar 11, 2004||The Board Of Trustees Of The University Of Illinois||Solids supporting mass transfer for fuel cells and other applications and solutions and methods for forming|
|US20040067402 *||Oct 2, 2003||Apr 8, 2004||Barndad Bahar||Ultra-thin integral composite membrane|
|US20040071881 *||Oct 9, 2002||Apr 15, 2004||Ballard Power Systems Inc.||Method and apparatus for the continuous coating of an ion-exchange membrane|
|US20040081876 *||Oct 14, 2003||Apr 29, 2004||Fenton James M.||Membrane electrode assemblies using ionic composite membranes|
|US20040081880 *||Oct 15, 2003||Apr 29, 2004||Samsung Electronics Co., Ltd.||Method for fabricating membrane-electrode assembly and fuel cell adopting the membrane-electrode assembly|
|US20040101743 *||Nov 20, 2003||May 27, 2004||Yasushi Sugawara||Polymer electrolyte fuel cell and preparation method for polymer electrolyte fuel cell|
|US20040106034 *||Nov 26, 2003||Jun 3, 2004||Bekkedahl Timothy A.||Fuel cell having a hydrophilic substrate layer|
|US20040110060 *||Dec 2, 2003||Jun 10, 2004||Toyota Jidosha Kabushiki Kaisha||Membrane-electrode assembly and production method thereof|
|US20040127347 *||Jun 13, 2003||Jul 1, 2004||Samsung Sdi Co., Ltd.||Method for manufacturing fuel cell electrode|
|US20040137283 *||Oct 20, 2003||Jul 15, 2004||Johna Leddy||Magnetically modified electrodes containing at least one catalyst component that mediates a subatomic particle transfer process|
|US20040241063 *||Jun 29, 2004||Dec 2, 2004||The Texas A&M University System||Fuel cell with monolithic flow field-bipolar plate assembly and method for making and cooling a fuel cell stack|
|US20040258979 *||Jun 20, 2003||Dec 23, 2004||Ballard Power Systems Inc.||Method of making a membrane electrode assembly for electrochemical fuel cells|
|US20050072514 *||Oct 6, 2003||Apr 7, 2005||Yan Susan G.||Method of making membrane electrode assemblies|
|US20050163920 *||Jan 22, 2004||Jul 28, 2005||Yan Susan G.||Membrane electrode assembly prepared by direct spray of catalyst to membrane|
|US20050181256 *||Nov 12, 2004||Aug 18, 2005||Shuguang Cao||Ion conductive random copolymers|
|US20050227855 *||Apr 7, 2004||Oct 13, 2005||Judith Manco||Method of making an electrode for a membrane electrode assembly and method of making the membrane electrode assembly|
|US20060029841 *||Aug 9, 2004||Feb 9, 2006||Engelhard Corporation||High surface area, electronically conductive supports for selective CO oxidation catalysts|
|US20060110631 *||Feb 18, 2005||May 25, 2006||Polyfuel, Inc.||Catalyst ink, process for making catalyst ink and for preparing catalyst coated membranes|
|US20060177726 *||Feb 6, 2006||Aug 10, 2006||Ji-Rae Kim||Fuel cell|
|US20060216564 *||Mar 15, 2006||Sep 28, 2006||Vincenzo Arcella||CCM composite|
|US20060237034 *||Apr 20, 2005||Oct 26, 2006||Lawrence Shore||Process for recycling components of a PEM fuel cell membrane electrode assembly|
|US20060240311 *||Mar 30, 2004||Oct 26, 2006||Holger Dziallas||Membrane-electrode unit for direct methanol fuel cells and method for the production thereof|
|US20070134407 *||Dec 12, 2006||Jun 14, 2007||Byd Company Limited||Fabrication methods for catalyst coated membranes|
|US20070175584 *||Dec 27, 2006||Aug 2, 2007||Solvay Solexis S.P.A.||Process for obtaining CCM with subgaskets|
|US20070227650 *||Jun 13, 2007||Oct 4, 2007||Yan Susan G||Method of making membrane electrode assemblies|
|US20070292745 *||Jun 20, 2006||Dec 20, 2007||Lawrence Shore||Process for recycling components of a PEM fuel cell membrane electrode assembly|
|US20080251205 *||Oct 12, 2006||Oct 16, 2008||Byd Company Limited||Method for Preparing a Membrane Electrode of a Fuel Cell|
|US20080280165 *||Jan 21, 2005||Nov 13, 2008||Toyota Jidosha Kabushiki Kaisha||Fuel Cell Cathode and a Polymer Electrolyte Fuel Cell Having the Same|
|US20080305250 *||Dec 12, 2006||Dec 11, 2008||Byd Company Limited||Fabrication Methods for Catalyst Coated Membranes|
|US20090206194 *||Feb 14, 2008||Aug 20, 2009||Lockheed Martin||Airship photocatalytic reactor energy generation, storage, and transmission systems|
|US20100035124 *||Aug 11, 2008||Feb 11, 2010||Gm Clobal Technology Operations, Inc.||Hybrid particle and core-shell electrode structure|
|US20100209815 *||Apr 28, 2010||Aug 19, 2010||Kent State University||Nanostructured core-shell electrocatalysts for fuel cells|
|US20100323273 *||Aug 22, 2008||Dec 23, 2010||Toyota Motor Engineering & Manufacturing North America, Inc.||Fuel cell electrodes with traizole modified polymers and membrane electrode assemblies incorporating same|
|US20110039178 *||Oct 14, 2010||Feb 17, 2011||Bekkedahl Timothy A||Fuel cell having a hydrophilic substrate layer|
|US20110052798 *||Sep 24, 2010||Mar 3, 2011||Solvay Solexis S.P.A.||Ccm composite|
|US20110207015 *||Apr 25, 2011||Aug 25, 2011||Toyota Motor Engineering & Manufacturing North America, Inc.||Fuel cell electrodes with triazole modified polymers and membrane electrode assemblies incorporating same|
|US20110212386 *||Nov 6, 2009||Sep 1, 2011||Justin Roller||Catalytic materials for fuel cell electroded and method for their production|
|US20130196245 *||Sep 30, 2010||Aug 1, 2013||Shampa Kandoi||Hot pressed, direct deposited catalyst layer|
|US20160301092 *||Mar 23, 2016||Oct 13, 2016||Samsung Sdi Co., Ltd.||Polymer electrolyte membrane for fuel cell and membrane-electrode assembly for fuel cell including same|
|USRE37307||Aug 20, 1998||Aug 7, 2001||W. L. Gore & Associates, Inc.||Ultra-thin integral composite membrane|
|USRE37433||Dec 17, 1999||Nov 6, 2001||E. I. Du Pont De Nemours And Company||Electrochemical conversion of anhydrous hydrogen halide to halogen gas using a membrane-electrode assembly or gas diffusion electrodes|
|CN1327555C *||Apr 14, 2004||Jul 18, 2007||清华大学||Self-breathing portable power supply|
|CN100474669C||May 21, 2003||Apr 1, 2009||三星Sdi株式会社||Film electrode module of fuel cell and preparing method thereof and fuel cell using the film electrode module|
|CN100517820C||Dec 16, 2005||Jul 22, 2009||中国科学院大连化学物理研究所||Ordered membrane electrode of proton-exchange membrane fuel battery, preparation and application thereof|
|DE10357223B4 *||Dec 8, 2003||Mar 20, 2008||Toyota Jidosha Kabushiki Kaisha, Toyota||Herstellungsverfahren für eine Membranelektroden-Anordnung|
|DE102007028007A1 *||Jun 14, 2007||Dec 24, 2008||BLüCHER GMBH||Brennstoffzelle mit Katalysator und deren Verwendung|
|EP0718903A1||Dec 7, 1995||Jun 26, 1996||Japan Gore-Tex, Inc.||An ion exchange membrane and electrode assembly for an electrochemical cell|
|EP0878860A1 *||May 12, 1998||Nov 18, 1998||Mazda Motor Corporation||Polymer electrolyte fuel cell with internal humidification|
|EP0945910A3 *||Mar 9, 1999||Jan 7, 2004||Umicore AG & Co. KG||Membrane electrode assembly for polymer-electrolyte fuel cell and method for its manufacture|
|EP1531509A1 *||Nov 6, 2003||May 18, 2005||Ballard Power Systems Inc.||Method and apparatus for the continuous coating of an ion-exchange membrane|
|EP1963013A1 *||Dec 12, 2006||Sep 3, 2008||Byd Company Limited||Fabrication methods for catalyst coated membranes|
|EP1963013A4 *||Dec 12, 2006||Jan 7, 2009||Byd Co Ltd||Fabrication methods for catalyst coated membranes|
|WO1995020691A1 *||Jan 26, 1995||Aug 3, 1995||United Technologies Corporation||High performance electrolytic cell electrode structures and a process for preparing such electrode structures|
|WO1997023920A1 *||Dec 11, 1996||Jul 3, 1997||Marchetti George A||A hydrophilic, graphite fuel cell electrode for use with an ionomer membrane and method of making a fuel cell|
|WO2000036679A1 *||Dec 16, 1999||Jun 22, 2000||The Regents Of The University Of California||Fuel cell anode configuration for co tolerance|
|WO2001074710A1 *||Mar 30, 2001||Oct 11, 2001||Manhattan Scientifics, Inc.||Portable chemical hydrogen hydride system|
|WO2002091504A1 *||Apr 22, 2002||Nov 14, 2002||The Regents Of The University Of California||Fuel cell anode configuration for co tolerance|
|WO2005081352A1 *||Feb 18, 2005||Sep 1, 2005||Polyfuel, Inc.||Catalyst ink, process for making catalyst ink and for preparing catalyst coated membranes|
|WO2007041962A1 *||Oct 12, 2006||Apr 19, 2007||Byd Company Limited||A method for preparing a membrane electrode of a fuel cell|
|WO2007048712A2 *||Oct 12, 2006||May 3, 2007||Basf Se||Surface-structured membranes and membranes coated with a catalyst, and membrane electrode units made therefrom|
|WO2007048712A3 *||Oct 12, 2006||Jun 21, 2007||Basf Ag||Surface-structured membranes and membranes coated with a catalyst, and membrane electrode units made therefrom|
|WO2007068199A1||Dec 12, 2006||Jun 21, 2007||Byd Company Limited||Fabrication methods for catalyst coated membranes|
|WO2012088176A1 *||Dec 20, 2011||Jun 28, 2012||E. I. Du Pont De Nemours And Company||High molecular weight ionomers and ionically conductive compositions for use as one or more electrode of a fuel cell|
|WO2017176306A1||Aug 2, 2016||Oct 12, 2017||Dioxide Materials, Inc.||Catalyst layers and electrolyzers|
|WO2017176597A1||Mar 31, 2017||Oct 12, 2017||Dioxide Materials, Inc.||Catalyst layers and electrolyzers|
|U.S. Classification||429/490, 427/115, 429/535, 429/524, 429/492|
|International Classification||H01M4/92, H01M8/10|
|Cooperative Classification||H01M2300/0082, H01M8/1004, H01M4/926|
|European Classification||H01M4/92S2, H01M8/10B2|
|Sep 9, 1991||AS||Assignment|
Owner name: UNITED STATES OF AMERICA, THE, AS REPRESENTED BY T
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:WILSON, MAHLON S.;REEL/FRAME:005828/0616
Effective date: 19910724
|Jan 15, 1993||AS||Assignment|
Owner name: REGENTS OF THE UNIVERSITY OF CALIFORNIA, THE, NEW
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:UNITED STATES DEPARTMENT OF ENERGY;REEL/FRAME:006388/0050
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|May 18, 2006||AS||Assignment|
Owner name: LOS ALAMOS NATIONAL SECURITY, LLC, NEW MEXICO
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